Summary of the invention
The object of the present invention is to provide a kind of water-based Stripable paint, mainly solve the problem existing for above-mentioned prior art, innovative point of the present invention is to add any auxiliary agent, resin self high cohesion is achieved with from the special polymerization technique of wound and raw material, the feature of low sticking power, and water-acid resistance excellent property, and have certain snappiness and elasticity, realizes that self is peelable.
For achieving the above object, the present invention realizes like this.
A kind of water-based Stripable paint, its manufacturing process is as follows:
A reactor technique:
A1 Polycondensation Reactor and Esterification Reactor adds water 18-23 weight part, and opens and stir;
A2 adds emulsifying agent 0.35-0.5 weight part and sodium lauryl sulphate 0.1 weight part; Wherein: the emulsifying agent of this step is sieve sub-rs-610 in ground and water according to adding amp-95 after mass ratio 1:9 agitation and dilution and ammoniacal liquor regulates ph to 8 to make;
A3 adds into vinylbenzene 2-4 weight part and methyl methacrylate 2 weight part;
A4 use water 3-4 weight part rinses reinforced container, and wash-down water all enters still;
A5 starts to heat up, until 85 DEG C;
B emulsion tank technique
B1 claims water 13-15 weight part to pour emulsion tank into;
B2 adds diacetone-acryloamide(DAA) 0.4-0.8 weight part and n-methylolacrylamide 0.2-0.4 weight part is to be dissolved;
B3 adds the emulsifying agent 0.35-0.5 weight part oneself modulated after dissolving, and stirs 5min; To be sieve sub-rs-610 in ground and water be in harmonious proportion ph to 7 make according to adding amp-95 and ammoniacal liquor after mass ratio 1:9 agitation and dilution for the emulsifying agent of this step;
B4, after material loading fully mixes, starts to add vinylformic acid 1-1.5 weight part, methyl methacrylate 11-13 weight part, butyl acrylate 14-16 weight part, vinylbenzene 7-8 weight part, ethyl propenoate 1.5-2.5 weight part, hydroxyethyl methacrylate 1-1.2 weight part;
B5 stirs 20min, puts stand-by on one side;
C reactive moieties:
When C1 temperature of reaction kettle is increased to 80-90 DEG C, add initiator; This initiator is in harmonious proportion by ammonium persulphate 0.2-0.24 weight part and water 6-7 weight part to form, and its consumption is 1/5 of initiator total amount;
After C2 adds initiator, when temperature rises to about 90 DEG C, open water of condensation, make temperature be kept for no more 92 DEG C, turn off water of condensation; Temperature of reaction kettle is made naturally to be reduced to 82-85 DEG C;
C3 temperature-stable after 40min starts to drip remaining initiator to 82-85 DEG C, drips pre-emulsification monomer prepared by step B subsequently, time for adding 220-260min;
C4 until both dropwise after, be incubated 85 DEG C continue 1 hour;
After C5 is incubated 1 hour, be cooled to 70 DEG C; Stablize after 70 DEG C, start aftertreatment;
D aftertreatment part:
D1 adds tertbutyl peroxide 0.04-0.06 weight part and enters still, and stirs 10min;
D2 adds Trisodium Citrate 0.03-0.04 weight part and is in harmonious proportion with water 0.5-0.8 weight part, enters still;
D3 enters still and stirs 10min, is cooled to 45 DEG C, adds the ammoniacal liquor of 10%-25% concentration, regulates ph to 7-8;
D4 adds adipic dihydrazide 0.3-0.36 weight part and water 1-1.5 weight part after stirring 10min, and filters discharging after stirring 10min.
By aforesaid method step, the ACRYLIC EMULSION finally making solid content 40-45%, 100-120 weight part of the water-based Stripable paint finally made.
In formula system of the present invention, pass through particle design, use daam(diacetone-acryloamide(DAA)) and adh(adipic dihydrazide) form crosslinking structure, make emulsion particle force of cohesion and macromole polarity very strong and be difficult to wetting base material, so very weak to the general sticking power of base material.For dry film 0.4mm, its 180 ° of stripping strengths on galvanized iron sheet are only 0.147kN/m, and the sticking power that its 180 ° of stripping strengths on ABS plate are only 0.147kN/m film is not high, peels off difficulty little.
Using method of the present invention is: can carry out technique initialization according to the difference on protected surface when emulsion is modulated into strippable paint, can showering, dip-coating, spraying, brushing.Suggestion big area burnishing surface uses.When film forming thickness reaches certain thickness, light stripping (first open an osculum on border, more whole being torn) after film forming drying, can be realized.
Compared with prior art advantage of the present invention is as follows:
1, decrease the interpolation of auxiliary agent, improve the stability of resin itself.
2, versatility is good, can be applicable to various base material, comprises the basal planes such as baking vanish face, plastics, cast iron, galvanized sheet, tinplate.
3, decrease the discharge of VOC, in resin paint process, volatile organic matter addition is no more than 6% of lacquering quality, and reach the strippable paint of 30% compared to auxiliary agent and amount of solvent easily, VOC greatly reduces, significant to environmental protection.
4, cost is low.Material cost is 7-8 unit/kg, and lacquering (quality is than accounting more than 85% in lacquering for main body emulsion resin, if do not add mill base, main body emulsion resin can accounting 95% or more) cost is less than 15 yuan/kg.Far below aqueous polyurethane on market or the provisional protective cover of oiliness, on market, the e-251 price of the peelable polyaminoester emulsion of main flow such as DSM is 45-50 unit/kg.
Embodiment
Embodiment 1
A kind of water-based Stripable paint, its manufacturing process is as follows:
A reactor technique:
A1 Polycondensation Reactor and Esterification Reactor adds water 18 weight parts, and opens and stir;
A2 adds emulsifying agent 0.35 weight part and sodium lauryl sulphate 0.1 weight part; Wherein: the emulsifying agent of this step is sieve sub-rs-610 in ground and water according to adding amp-95 after mass ratio 1:9 agitation and dilution and ammoniacal liquor regulates ph to 8 to make;
A3 adds into vinylbenzene 2 weight part and methyl methacrylate 2 weight part;
A4 use water 3 weight part rinses reinforced container, and wash-down water all enters still;
A5 starts to heat up, until 85 DEG C;
B emulsion tank technique
B1 claims water 13 weight part to pour emulsion tank into;
B2 adds diacetone-acryloamide(DAA) 0.4 weight part and n-methylolacrylamide 0.2 weight part is to be dissolved;
B3 adds emulsifying agent 0.35 weight part oneself modulated after dissolving, and stirs 5min; To be sieve sub-rs-610 in ground and water be in harmonious proportion ph to 7 make according to adding amp-95 and ammoniacal liquor after mass ratio 1:9 agitation and dilution for the emulsifying agent of this step;
B4, after material loading fully mixes, starts to add vinylformic acid 1 weight part, methyl methacrylate 11 weight part, butyl acrylate 14 weight part, vinylbenzene 7 weight part, ethyl propenoate 1.5 weight part, hydroxyethyl methacrylate 1 weight part;
B5 stirs 20min, puts stand-by on one side;
C reactive moieties:
When C1 temperature of reaction kettle is increased to 80 DEG C, add initiator; This initiator is in harmonious proportion by ammonium persulphate 0.2 weight part and water 6 weight part to form, and its consumption is 1/5 of initiator total amount;
After C2 adds initiator, when temperature rises to about 90 DEG C, open water of condensation, make temperature be kept for no more 92 DEG C, turn off water of condensation; Temperature of reaction kettle is made naturally to be reduced to 82 DEG C;
C3 temperature-stable to 82 DEG C after 40min starts to drip remaining initiator, drips pre-emulsification monomer prepared by step B subsequently, time for adding 220min;
C4 until both dropwise after, be incubated 85 DEG C continue 1 hour.
After C5 is incubated 1 hour, be cooled to 70 DEG C; Stablize after 70 DEG C, start aftertreatment;
D aftertreatment part:
D1 adds tertbutyl peroxide 0.04 weight part and enters still, and stirs 10min;
D2 adds Trisodium Citrate 0.03 weight part and is in harmonious proportion with water 0.5-0.8 weight part, enters still;
D3 enters still and stirs 10min, is cooled to 45 DEG C, adds the ammoniacal liquor of 10% concentration, regulates ph to 7;
D4 adds adipic dihydrazide 0.3 weight part and water 1 weight part after stirring 10min, and filters discharging after stirring 10min.
During use, with spraying method, water-based Stripable paint is coated on PVC plastic panel, light stripping (first open an osculum on border, more whole being torn) after film forming drying, can be realized.
Embodiment 2
A kind of water-based Stripable paint, its manufacturing process is as follows:
A reactor technique:
A1 Polycondensation Reactor and Esterification Reactor adds water 23 weight parts, and opens and stir;
A2 adds emulsifying agent 0.5 weight part and sodium lauryl sulphate 0.1 weight part; Wherein: the emulsifying agent of this step is sieve sub-rs-610 in ground and water according to adding amp-95 after mass ratio 1:9 agitation and dilution and ammoniacal liquor regulates ph to 8 to make;
A3 adds into vinylbenzene 4 weight part and methyl methacrylate 2 weight part;
A4 use water 4 weight part rinses reinforced container, and wash-down water all enters still;
A5 starts to heat up, until 85 DEG C;
B emulsion tank technique
B1 claims water 15 weight part to pour emulsion tank into;
B2 adds diacetone-acryloamide(DAA) 0.8 weight part and n-methylolacrylamide 0.4 weight part is to be dissolved;
B3 adds emulsifying agent 0.5 weight part oneself modulated after dissolving, and stirs 5min; To be sieve sub-rs-610 in ground and water be in harmonious proportion ph to 7 make according to adding amp-95 and ammoniacal liquor after mass ratio 1:9 agitation and dilution for the emulsifying agent of this step;
B4, after material loading fully mixes, starts to add vinylformic acid 1.5 weight part, methyl methacrylate 13 weight part, butyl acrylate 16 weight part, vinylbenzene 8 weight part, ethyl propenoate 2.5 weight part, hydroxyethyl methacrylate 1.2 weight part;
B5 stirs 20min, puts stand-by on one side;
C reactive moieties:
When C1 temperature of reaction kettle is increased to 90 DEG C, add initiator; This initiator is in harmonious proportion by ammonium persulphate 0.24 weight part and water 7 weight part to form, and its consumption is 1/5 of initiator total amount;
After C2 adds initiator, when temperature rises to about 90 DEG C, open water of condensation, make temperature be kept for no more 92 DEG C, turn off water of condensation; Temperature of reaction kettle is made naturally to be reduced to 85 DEG C;
C3 temperature-stable to 85 DEG C after 40min starts to drip remaining initiator, drips pre-emulsification monomer prepared by step B subsequently, time for adding 260min;
C4 until both dropwise after, be incubated 85 DEG C continue 1 hour.
After C5 is incubated 1 hour, be cooled to 70 DEG C; Stablize after 70 DEG C, start aftertreatment;
D aftertreatment part:
D1 adds tertbutyl peroxide 0.06 weight part and enters still, and stirs 10min;
D2 adds Trisodium Citrate 0.04 weight part and is in harmonious proportion with water 0.8 weight part, enters still;
D3 enters still and stirs 10min, is cooled to 45 DEG C, adds the ammoniacal liquor of 25% concentration, regulates ph to 8;
D4 adds adipic dihydrazide 0.36 weight part and water 1.5 weight part after stirring 10min, and filters discharging after stirring 10min.
During use, in the mode of brushing, water-based Stripable paint is coated on tinplate on the surface, light stripping (first open an osculum on border, more whole being torn) after film forming drying, can be realized.
Embodiment 3
A kind of water-based Stripable paint, its manufacturing process is as follows:
A reactor technique:
A1 Polycondensation Reactor and Esterification Reactor adds water 20 weight parts, and opens and stir;
A2 adds emulsifying agent 0.4 weight part and sodium lauryl sulphate 0.1 weight part; Wherein: the emulsifying agent of this step is sieve sub-rs-610 in ground and water according to adding amp-95 after mass ratio 1:9 agitation and dilution and ammoniacal liquor regulates ph to 8 to make;
A3 adds into vinylbenzene 3 weight part and methyl methacrylate 2 weight part;
A4 use water 3.5 weight part rinses reinforced container, and wash-down water all enters still;
A5 starts to heat up, until 85 DEG C;
B emulsion tank technique
B1 claims water 14 weight part to pour emulsion tank into;
B2 adds diacetone-acryloamide(DAA) 0.6 weight part and n-methylolacrylamide 0.3 weight part is to be dissolved;
B3 adds the emulsifying agent 0.35-0.5 weight part oneself modulated after dissolving, and stirs 5min; To be sieve sub-rs-610 in ground and water be in harmonious proportion ph to 7 make according to adding amp-95 and ammoniacal liquor after mass ratio 1:9 agitation and dilution for the emulsifying agent of this step;
B4, after material loading fully mixes, starts to add vinylformic acid 1.2 weight part, methyl methacrylate 12 weight part, butyl acrylate 15 weight part, vinylbenzene 8 weight part, ethyl propenoate 2 weight part, hydroxyethyl methacrylate 1.2 weight part;
B5 stirs 20min, puts stand-by on one side;
C reactive moieties:
When C1 temperature of reaction kettle is increased to 85 DEG C, add initiator; This initiator is in harmonious proportion by ammonium persulphate 0.3 weight part and water 6 weight part to form, and its consumption is 1/5 of initiator total amount;
After C2 adds initiator, when temperature rises to about 90 DEG C, open water of condensation, make temperature be kept for no more 92 DEG C, turn off water of condensation; Temperature of reaction kettle is made naturally to be reduced to 85 DEG C;
C3 temperature-stable to 85 DEG C after 40min starts to drip remaining initiator, drips pre-emulsification monomer prepared by step B subsequently, time for adding 250min;
C4 until both dropwise after, be incubated 85 DEG C continue 1 hour.
After C5 is incubated 1 hour, be cooled to 70 DEG C; Stablize after 70 DEG C, start aftertreatment;
D aftertreatment part:
D1 adds tertbutyl peroxide 0.05 weight part and enters still, and stirs 10min;
D2 adds Trisodium Citrate 0.03 weight part and is in harmonious proportion with water 0.7 weight part, enters still;
D3 enters still and stirs 10min, is cooled to 45 DEG C, adds the ammoniacal liquor of 20% concentration, regulates ph to 8;
D4 adds adipic dihydrazide 0.35 weight part and water 1.5 weight part after stirring 10min, and filters discharging after stirring 10min.
During use, with dip coating manner, water-based Stripable paint is coated on the surface of ironcasting, light stripping (first open an osculum on border, more whole being torn) after film forming drying, can be realized.
Be only preferred embodiment of the present invention in sum, be not used for limiting practical range of the present invention.Namely all equivalences done according to the content of the present patent application the scope of the claims change and modify, and all should be technology category of the present invention.